TECHNICAL FIELD
[0001] The present invention relates to a lithium ion secondary battery. More particularly,
it relates to a lithium ion secondary battery which has a high capacity, rapid charge
and discharge characteristics, a high flatness of charge and discharge potential,
and an excellent cycle performance.
BACKGROUND ART
[0002] With a recent tendency toward smaller size of electronic devices, necessity is rising
for the enhancement of capacity of secondary batteries used for such electronic devices.
Accordingly, attention has been focused on lithium ion secondary batteries having
higher energy density than the conventional nickel/cadmium batteries or nickel/hydrogen
batteries. It was initially tried to use lithium metal as negative electrode material
of such batteries.
[0003] However, in case of lithium ion secondary batteries, it was found that dendrite-like
lithium separates out in repetition of charge and discharge and passes through the
separator to reach the positive electrode, causing a risk of short circuiting and
consequent firing of the battery. Therefore, attention has been focused on lithium
battery in which shifting of the non-aqueous solvent in the process of charge and
discharge takes place between the layers, and carbonaceous materials capable of preventing
separation of lithium metal are used as negative electrode material.
[0004] In Japanese Patent Application Laid-Open (KOKAI) No. 57-208079, there is proposed
the use of graphite as the said carbonaceous material. When graphite having high crystallinity
is used as negative carbon electrode material of a lithium ion secondary battery,
there can be obtained a battery capacity close to 372 mAh/g which is closed to the
theoretical capacity of lithium occlusion of graphite. However, since graphite is
active to the electrolyte, there is generally observed an irreversible capacity of
not less than several ten mAh/g due to layer formation or side reactions in the initial
cycle of charge and discharge.
[0005] X-ray diffractometry has been used for determining crystallinity of graphite. This
method is suited for observing the difference in properties of the carbonaceous materials
due, for one thing, to different calcination temperatures, but inadequate for determining
the difference between the carbonaceous materials, especially for classifying the
high-crystallinity graphite materials. For instance, the parameter (d002) of the carbon
layer interplanar spacing that can be determined by X-ray diffractometry is limited
to the range of 3.357 to 3.360 Å for the high-crystallinity graphite materials, which
represents no significant difference between such materials. Also, "La" which indicates
the crystallite size in the basal direction of carbon and "Lc" indicating the crystallite
size in the laminating direction of carbon, that can be determined by X-ray diffractometry,
are outside the limits of determination for high-crystallinity graphite, so that it
is impossible with this method to make a correct comparison of the materials.
[0006] On the other hand, the capacity of low-temperature calcined amorphous carbon, which
is more than the theoretical capacity of graphite, can be increased up to about 500
mAh/g by proper setting of cut-off potential. In this case, however, because of excessively
high potential at the time of undoping of lithium ions as compared with that of graphite,
and also because of a large hysteresis in potential characteristics between charge
and discharge, it is quite difficult to produce a potential difference from the positive
electrode, making it unable to obtain a large-capacity and high-powder battery. A
large loss of capacity that occurs in the initial cycle of charge and discharge is
also a baffling problem, and further, it is known that a sharp drop of capacity takes
place on rapid charging.
[0007] LiNiO
2 is a hopeful candidate for positive electrode material of lithium ion secondary batteries
because this material is more excellent than LiCoO
2, which has hitherto been popularly used as positive electrode active material, in
capacity and cost as well as in the aspect of reserves of its raw material, but this
material involves the problem that as it is lower in potential against Li/Li
+ than LiCoO
2, it is difficult to produce a potential difference from the negative electrode.
[0008] It is, therefore, considered that in order to make the best use of the advantages
of LiNiO
2, development of a negative electrode material capable of providing a high capacity
at a potential close to 0 V against Li/Li
+ is essential.
[0009] In certain uses of lithium ion secondary batteries, for example, in use thereof for
the electric automobiles, it is likely that there arises an occasion where quick recharging
is required. In such uses, an electrode material with excellent rate characteristics
is needed.
[0010] The present invention has been made in consideration of the above circumstances,
and it is an object to provide a lithium ion secondary battery which has a high capacity,
rapid charge and discharge characteristics, a high flatness of charge and discharge
potential, and a good cycle performance.
DISCLOSURE OF INVENTION
[0011] As a result of the present inventors' earnest studies, it has been found that a negative
electrode capacity and a rate characteristics against high-speed charge and discharge
can be estimated from the results of determination of a particle size of the graphite
used as a negative electrode material, a BET specific surface area and Raman parameters
by Raman spectroscopic analysis thereof, before actually applying various types of
graphite material as a negative electrode for a lithium ion secondary battery and
determining various electrochemical properties such as electrode capacity.
[0012] The present inventors also have found that among many powdery graphite materials,
those having excellent rate characteristics against a negative electrode capacity
and a high-speed charge and discharge are limited to the materials whose numerical
values of the above determinations fall within a certain specified range, and the
said materials are either (a) high-crystallinity natural or artificial graphite or
(b) natural, artificial or expanded graphite subjected to re-heat treatment at a temperature
of not lower than 2,000°C.
[0013] The present inventors have further found that when the surface of a graphitic carbonaceous
material is coated with a carbonizable organic material, then calcined, pulverized
and treated with an acid or alkaline solution, it is possible to provide a higher
capacity than before treatment, and as compared with the case where amorphous carbon
is used, the potential at the time of lithium doping or undoping remains close to
the potential of Li/Li
+ like graphite. Moreover, the said carbonaceous material has no potential hysteresis
due to charge and discharge, and it is easy to produce a potential difference from
the positive electrode, so that a high working efficiency can be realized from the
first cycle of charge and discharge. Further, the said treated carbonaceous material
is improved in rate characteristics.
[0014] The present invention has been attained on the basis of the above findings, and its
essential aspect comprises the following embodiments:
(1) A lithium ion secondary battery comprising a positive electrode, a non-aqueous
electrolyte, a separator and a negative electrode comprising a carbonaceous material
capable of charging and discharging lithium ions, the said negative electrode containing
at least one type of graphite material which satisfies the conditions specified in
the following (a) and (b):
(a) when the BET specific surface area of the graphite material is represented by
"y" (m2/g) and the particle size by "x" (µm), the material falls within the region defined
by the following formula (I):

(b) In Raman spectroscopic analysis using argon ion laser light with a wavelength
of 5,145 Å, the ratio of the strength of the peak existing in the region of 1,350-1,370
cm-1 (IB) to the strength of the peak existing in the region of 1,570-1,620 cm-1 (IA), which is represented by an R value (IB/IA), falls in the range of 0.001 to
0.2.
(2) A lithium ion secondary battery characterized by using as negative electrode,
an "amorphous carbon-coated graphitic carbonaceous material" prepared by coating the
particle surfaces of the graphite material described in (1) above with a carbonizable
organic material, and calcining and pulverizing the coated material.
(3) A lithium ion secondary battery characterized by using as negative electrode a
graphite material prepared by coating the surfaces of a graphite material with a carbonizable
organic material, calcining and pulverizing the coated material, and then treating
it with an acid or alkaline solution.
(4) A lithium ion secondary battery characterized by using as negative electrode a
graphite material prepared by coating the surfaces of the graphite material as defined
in (1) above with a carbonizable organic material, calcining and pulverizing the coated
material, and then treating it with an acid or alkaline solution.
[0015] The present invention is describe in detail below.
[0016] First, the materials used in the present invention are explained.
A. Graphite material
[0017] The graphite powder used in the present invention is preferably selected from (1)
high-crystallinity natural or artificial graphite, (2) natural, artificial or expanded
graphite subjected to re-heat treatment at not lower than 2,000°C and (3) highly purified
products of these graphite materials, as far as their properties are known.
[0018] In case of using graphitized materials having same qualities as (1) or (2), obtained
by graphitizing the graphitizable materials, the following graphitizable materials
can be cited: (4) graphitized materials obtained by calcining at 2,500-3,200°C one
or more of the organic materials selected from the group consisting of coal tar pitch,
coal heavy oil, normal pressure residual oil, petroleum heavy oil, aromatic hydrocarbons,
nitrogen-containing cyclic compounds, sulfur-containing cyclic compounds, polyphenylene,
polyvinyl chloride, polyvinyl alcohol, polyacrylonitrile, polyvinyl butyral, natural
polymers, polyphenylene sulfide, polyphenylene oxide, furfuryl alcohol resins, phenol-formaldehyde
resins and imide resins, (5) graphitized materials obtained by calcining the graphitizable
materials such as shown in the above (4) usually at 400-2,500°C, preferably at 1,000-2,000°C,
in the presence of a catalyst such as powder or thin film of at least one material
selected from the group consisting of lithium, beryllium, boron, magnesium, aluminum,
silicon, potassium, calcium, titanium, vanadium, chromium, manganese, copper, zinc,
nickel, platinum, palladium, cobalt, ruthenium, tin, lead, iron, germanium, zirconium,
molybdenum, silver, barium, tantalum, tungsten and rhenium.
[0019] The graphite materials which are unable to satisfy the said conditions of (a) and
(b) specified in the present invention can also be used if they are subjected to re-calcination
treatment at 2,000-3,200°C so that they meet the conditions of (a) and (b).
B. Determination of graphite material
[0020]
(i) First, the particle size is measured. Any preferable method such as a laser diffractometry
method, an electric resistance method or a direct particle size determination method
comprising processing of a CCD high-sensitivity camera photographic image, can be
used for measurement of the particle size. Graphite powder having an average particle
diameter of 4-40 µm is selected.
(ii) Then the specific surface area is measured. The BET method by a gaseous molecular
adsorption, an organic molecular adsorption method, an organic solvent adsorption
method, etc., can be used for measuring the specific surface area. The graphite powders
having a particle size in the above-defined range are further screened to select those
whose BET specific surface area falls within the range of 0.1-25 m2/g.
(iii) These graphite powders are additionally screened to obtain the particles satisfying
the above-shown formula (I) defining the relation between the BET specific surface
area (m2/g) and a particle size (µm). Particularly the graphite material satisfying the following
formula (II), or the graphite material having an average particle size of 4-30 µm
and a BET specific surface area of 0.1-20 m2/g, is preferred:

(iv) Next, the graphite material satisfying the above relation between an average
particle size and a specific surface area is subjected to Raman spectroscopic analysis
using 5,145 Å argon ion laser light to select the material whose R value (IB/IA) (IA:
strength of the peak existing at 1,570-1,620 cm-1; IB: strength of the peak existing at 1,350-1,370 cm-1) falls within the range of 0.001 to 0.2. It is preferred to select a material whose
Δυ value, or half-value width of the peak existing at 1,570-1,620 cm-1, is in the range of 14 to 22 cm-1.
[0021] The R value is preferably in the range of 0.001 to 0.15, more preferably 0.001 to
0.07.
[0022] In the graphite material used in the present invention, the interplanar distance
(d002) of the (002) face in X-ray diffraction is preferably not more than 3.38 Å,
more preferably not more than 3.36 Å, and the crystallite size (Lc) in the direction
of the c-axis is preferably not more than 1,000 Å.
[0023] Japanese Patent Application Laid-Open (KOKAI) No. 7-235294 notes that there is a
problem of vigorous generation of gases when a graphite material with the R value
of not more than 0.20 is used.
[0024] According to the present invention, however, the possibility of such generation of
gases can be eliminated by using a graphite material satisfying the above-defined
conditions relating to the average particle size and the specific surface area, and
further, the properly selection of the electrolyte and the good design of the battery
structure makes it possible to obtain a battery having no such problem in practical
use.
[0025] Even better result can be obtained when using an "amorphous carbon-coated graphitic
carbonaceous material" obtained by coating the said graphite material with a carbonizable
organic material, calcining, carbonizing and pulverizing the coated graphite material.
C. "Amorphous carbon-coated graphitic carbonaceous material"
[0026] The "amorphous carbon-coated graphitic carbonaceous material" according to the present
invention is a material obtained by coating a base graphite material with a carbonizable
organic material, carbonizing the coated material by calcination, and pulverizing
the calcined material. This material has the property of occluding and releasing lithium
ions. More specifically, this powdery carbonaceous material is characterized by the
facts that the interplanar spacing (d002) of the carbon crystal is in the range of
3.35 to 3.39 Å, and that the R value of more than that of the base graphite material,
preferably falls within the range of 0.15 to 1.0, more preferably 0.2 to 0.5.
[0027] The above-defined material can be easily obtained by using, for example, the following
base materials.
D. Base graphite materials usable for preparing "amorphous carbon-coated graphitic
carbonaceous material"
[0028] The base graphite material used in the present invention may take optional shapes
such as globular, plate, fibrous, etc, and it has preferably such a shape that the
average particle size thereof is smaller than that of the "amorphous carbon-coated
graphitic carbonaceous material" after pulverization. Especially preferably, the material
has such a shape that its average particle size or average major diameter is in the
range of 20 to 99% of the average particle size of the "amorphous carbon-coated graphitic
carbonaceous material."
[0029] Preferred examples of such base graphite material are graphitized products of conductive
carbon black such as acetylene black and Ketchen black, powder of artificial or natural
graphite and its purified products, and carbon fiber such as vapor phase-grown carbon
fiber. Especially, a material which satisfies the above-defined conditions on relation
between the particle size and the specific surface area, the Raman R value and the
half-value width, is preferred.
E. Organic material for preparing "amorphous carbon-coated graphitic carbonaceous
material"
[0030]
(i) The organic materials which can be carbonized in liquid phase include coal heavy
oils such as various types of coal tar pitch ranging from soft pitch to hard pitch
and dry-distillation liquefied oil, and petroleum heavy oils, for example, straight
run heavy oils such as normal pressure residual oil and reduced pressure residual
oil, and cracked heavy oils such as ethylene tar which is formed as a by-product in
cracking of crude oil or naphtha. The said organic materials also include aromatic
hydrocarbons such as acenaphthylene, decacyclene and anthracene, nitrogen-containing
cyclic compounds such as phenazine and acridine, sulfur-containing cyclic compounds
such as thiophene, alicyclic compounds such as adamantane (these compounds need to
be pressed to not less than 30 MPa), and polymers such as polyphenylenes (biphenyl,
terphenyl, etc.), polyvinyl chloride and polyvinyl alcohol.
(ii) The organic materials which can be carbonized in solid phase, include natural
polymers such as cellulose and saccharides, thermoplastic resins such as polyphenylene
sulfide and polyphenylene oxide, and thermocuring resins such as furfuryl alcohol
resin, phenol-formaldehyde resin and imide resin.
F. Preparation of "amorphous carbon-coated graphitic carbonaceous material"
[0031] An "amorphous carbon-coated graphitic carbonaceous material" can be obtained by mixing
a lead material and an organic material such as mentioned above, calcining the mixture
usually at 400-2,800°C, preferably at 700-1,500°C, and pulverizing the calcined material.
The average particle size of the "amorphous carbon-coated graphitic carbonaceous material"
is usually in the range of 4 to 100 µm, preferably 5 to 50 µm.
[0032] The graphite content in the finally prepared "amorphous carbon-coated graphitic carbonaceous
material" is usually in the range of 50 to 99% by weight, preferably 75 to 99% by
weight, more preferably 90 to 99% by weight, and the content of the calcined organic
material is usually in the range of 1 to 50% by weight, preferably 1 to 25% by weight,
more preferably 1 to 10% by weight.
[0033] As for the properties of the said graphite particles, it is preferable that the interplanar
spacing (d002) of the (002) face in X-ray diffraction is in the range of 3.36 to 3.39
Å, the said R value is in the range of 0.15 to 1.0, and the BET specific surface area
is in the range of 0.1 to 13 m
2/g. The upper limit of the BET specific surface area is preferably 10 m
2/g, more preferably 4 m
2/g.
[0034] If the content of the calcined organic material exceeds the above-defined range,
there can not be sufficiently obtained the effects of lowering the potential and improving
the rapid charge/discharge characteristics. In this case, the effect of the acid or
alkali treatment, which is preferably conducted at a later stage for further improvement
of battery performance, is also poor.
[0035] The above-shown compositional range is the value not at the stage of supply of the
starting material but at the stage of final preparation. Therefore, when the material
is supplied, it is necessary to decide the amount of the material to be supplied in
consideration of the compositional ratio at the final stage. The lithium ion secondary
battery using the thus prepared "amorphous carbon-coated graphitic carbonaceous material"
for the negative electrode has a higher capacity and also shows more excellent rate
and cycle characteristics than the battery having its negative electrode composed
a non-coated graphite material.
G. Acid solution
[0036] The acid solution used for treating the "amorphous carbon-coated graphitic carbonaceous
material" in the present invention is not specified; it is possible to use, for instance,
the solutions of inorganic acids such as halogenous acids (hydrofluoric acid, hydrochloric
acid, bromic acid, iodic acid, etc.), sulfuric acid and nitric acid, organic acids
such as trichloroacetic acid, trifluoroacetic acid and oxalic acid, and mixtures of
these acids. It is preferred to use an acid solution heated at a temperature not higher
than the boiling point of water. The preferred acid solution for use in the present
invention is a solution of hydrochloric acid. The preferred range of concentration
of the acid solution is not less than 5 N (normal).
H. Alkaline solution
[0037] The alkaline solution used for treating the "amorphous carbon-coated graphitic carbonaceous
material" in the present invention is also not specified; it is possible to use, for
instance, the solutions of alkali metal hydroxides such as sodium hydroxide and potassium
hydroxide, solutions of ammonia, tetraalkylanmonium, urea and the like, and solutions
of organic amines such as pyridine, quinoline, quinoxaline and piperidine. It is preferred
to use an alkaline solution heated at a temperature not higher than the boiling point
of water The preferred alkaline solution for use in the present invention is a solution
of an alkali metal hydroxide. The preferred range of concentration of the alkaline
solution is not less than 5 N in the case of alkali metal hydroxides.
[0038] The method for producing the negative electrode according to the present invention
is described below.
[0039] The method for producing the negative electrode in the present invention is not subject
to specific restrictions as far as the said materials are used; for instance, the
following method can be used. Also, in the present invention, in case where such graphitic
material is coated with a carbonizable organic substance, then calcined, pulverized
and treated with an acid or alkaline solution, even the graphitic material having
no specific properties described above can be used preferably as a negative electrode
material.
[0040] First, by using a mixer having heating means, a graphite material and an organic
substance are mixed in such a ratio that the final composition become within the above-defined
range, and the mixture is subjected to a deaeration/devolatilization treatment and
calcined usually at 400 to 2,000°C for 0.1 to 12 hours, preferably at 700 to 1,500°C
for 0.5 to 5 hours. The calcination product is pulverized to obtain an "amorphous
carbon-coated graphitic carbonaceous material."
[0041] Then this "amorphous carbon-coated graphitic carbonaceous material" is dispersed
in an acid or alkaline solution and stirred, shaken or subjected to supersonic treatment
at 20 to 150°C for a period of preferably 0.5 hour to one week.
[0042] Then the acid or alkaline solution adhered to the particle is washed away with ultra-pure
water or distilled water, and the washed particles are dried. The drying temperature
is usually 80 to 350°C, preferably 80 to 150°C. There is no need of heating to such
a high temperature that may cause a change in the structure of the base carbon material.
[0043] The negative electrode material for the lithium ion secondary battery according to
the present invention has an amorphous carbon phase on the surface before it is reformed.
Therefore, after reformation with an acid or alkaline solution, it only needs to dry
the material at a temperature of 80 to 150°C after washing with water, with no high-temperature
heat-treatment required.
[0044] In a lithium ion secondary battery, the negative electrode comprising the "amorphous
carbon-coated graphitic carbonaceous material" subjected to an acid or alkali treatment
is capable of providing a higher battery capacity and also shows better rate and cycle
characteristics than possible with a negative electrode comprising the non-treated
"amorphous carbon-coated graphitic carbonaceous material."
[0045] Then, a binder and a solvent are added to the said graphite powder to form a slurry,
and this slurry is applied to a metallic collector substrate such as a copper foil
and dried to prepare to an electrode. The electrode material may be molded as is into
a form of electrode by such method as roll molding or compression molding. The same
operation may be applied for molding the positive electrode.
[0046] As the said binder, the polymers stable against the solvents are used. Examples of
such polymers include resinous polymers such as polyethylene, polypropylene, polyethylene
terephthalate, aromatic polyamides and cellulose, rubber-like polymers such as styrene-butadiene
rubber, isoprene rubber, butadiene rubber and ethylene-propylene rubber, thermoplastic
elastomeric polymers such as styrene-butadiene-styrene block copolymer and its hydrogenation
product, styrene-ethylene-butadiene-styrene copolymer, styrene-isoprene-styrene block
copolymer and its hydrogenation product, soft resinous polymers such as syndiotactic
1,2-polybutadiene, ethylene-vinyl acetate copolymer and propylene-α-olefin (C
2-C
12) copolymer, fluoro-polymers such as polyvinylidene fluoride, polytetrafluoroethylene
and polytetrafluoroethylene-ethylene copolymer, and polymer compositions having alkali
metal ion, particularly lithium ion conductivity.
[0047] The said polymers having ion conductivity include the following systems (i) and (ii):
(i) A system comprising a combination of a polyether-based polymer such as polyethylene
oxide or polypropylene oxide, a crosslinked polymer such as polyether compound, or
a high- molecular weight compound such as polyepichlorohydrin, polyphosphazene, polysiloxane,
polyvinyl pyrrolidone, polyvinylidenecarbonate or polyacrylonitrile, with a lithium
salt or a lithium-based alkali metal salt;
(ii) A system comprising a combination of an organic compound having high dielectric
constant, such as propylene carbonate, ethylene carbonate or γ-butyrolactone, with
the above system (i).
[0048] Ion conductivity of the said ion-conductive polymer compositions at room temperature
is usually not less than 10
-5 S/cm, preferably not less than 10
-3 S/cm.
[0049] Mixing form of a graphite material ("amorphous carbon-coated graphitic carbonaceous
material") and a binder may be various forms; for example, the particles of both materials
are mixed; a fibrous binder is mixed with the particles of the graphite material in
an entangled state; a layer of the binder adheres to the graphite material particle
surfaces.
[0050] The mixing percentage of the binder to the graphite material is usually 0.1 to 30%
by weight, preferably 0.5 to 10% by weight. When the mixing percentage of the binder
to the graphite material exceeds 30% by weight, the produced electrode has high internal
resistance, and when the said percentage is less than 0.1% by weight, bindability
of the carbonaceous powder to the collector tends to be poor.
[0051] The secondary battery of the present invention is here explained.
[0052] The secondary battery of the present invention comprises a combination of a negative
electrode plate obtained in the manner described above, an electrolyte and a positive
electrode plate described below, plus other battery elements such as separator, gaskets,
collector, cover plate and cell case.
[0053] The shape of the battery is not specified in the present invention; it may be, for
instance, cylindrical, square or coin-like. In the present invention, basically, a
collector and a negative electrode material are mounted on a cell floor plate, an
electrolyte and a separator are placed thereon, the positive electrode is mounted
in opposition to the negative electrode, and the assembly is caulked with gaskets
and a cover plate to constitute a secondary battery.
[0054] The non-aqueous solvents usable for the electrolyte in the present invention include
the organic solvents such as propylene carbonate, ethylene carbonate, chloroethylene
carbonate, trifluoropropylene carbonate, diethyl carbonate dimethyl carbonate, ethyl
methyl carbonate, 1,2-dimethoxyethane, γ-butyrolactone, tetrahydrofuran, 2-methyltetrahydrofuran,
sulphorane and 1,3-dioxorane. These solvents may be used either singly or as a mixture
of two or more of them. In the case of non-aqueous solvents described above, an additive
capable of forming a coating which enabled efficient charge and discharge of lithium
ions on the negative electrode surface may be added in an optional ratio. Examples
of such additives include gases such as CO
2, N
2O, CO and SO
2, polysulfide Sx
-2, vinylene carbonate, catechol carbonate and the like.
[0055] The electrolyte is prepared by adding an inorganic or organic lithium salt to a non-aqueous
solvent such as mentioned above. The inorganic lithium salts usable for this purpose
include LiClO
4, LiPF
6, LiBF
4, LiAsF
6, LiCl, LiBr and the like, and the organic lithium salts include LiCF
3SO
3, LiN(SO
2CF
3)
2, LiN(SO
2C
2F
5)
2, LiC(SO
2CF
3)
3, LiN(SO
3CF
3)
2 and the like.
[0056] It is also possible to use the polymeric solid electrolytes which are the conductors
of alkali metal ions such as lithium ions.
[0057] The positive electrode material is not specified in the present invention, but it
is preferred to use the metallic chalcogen compounds which are capable of occluding
and releasing the alkali metal cations such as lithium ions during charge and discharge.
Examples of such metallic chalcogen compounds include vanadium oxides, vanadium sulfides,
molybdenum oxides, molybdenum sulfides, manganese oxides, chromium oxides, titanium
oxides, titanium sulfides, and the composites of these oxides and sulfides. Preferred
among these compounds are Cr
3O
8, V
2O
5, V
5O
13, VO
2, Cr
2O
5, MnO
2, TiO
2, MoV
2O
8, TiS
2V
2S
5MoS
2, MoS
3VS
2, Cr
0.25V
0.75S
2, Cr
0.5V
0.5S
2 and the like.
[0058] It is also possible to use chalcogen compounds such as LiMY
2 (wherein M is a transition metal such as Co or Ni, and Y is O or S), oxides such
as LiM
2Y
4 (wherein M is Mn, and Y is O), sulfides such as CuS, Fe
0.25V
0.75S
2 and Na
0.1CrS
2, phosphorus and sulfur compounds such as NiPS
3 and FePS
3, and selenium compounds such as VSe
2 and NbSe
3.
[0059] The positive electrode is prepared by mixing a compound such as mentioned above with
a binder and coating it on a collector as in the case of the negative electrode.
[0060] The separator for retaining the electrolyte usually comprises a material having excellent
liquid holding property. For instance, a non-woven fabric or a porous film of a polyolefin
resin is impregnated with the said electrolyte.
BEST MODE FOR CARRYING OUT THE INVENTION
[0061] The present invention is hereinafter described in further detail by showing the examples
thereof, which examples however are merely intended to be illustrative and not to
be construed as limiting the scope of the invention.
(1) Evaluation of electrode materials
[0062] Particle size determination was made by using a laser diffraction type particle size
analyzer. The automatically calculated average particle size was used as standard
of evaluation.
[0063] The specific surface area was measured according to the BET one-point method.
[0064] Raman spectroscopy was conducted by irradiating 5,145 Å argon ion laser light at
an intensity of 30 mW using Nippon Bunko NR-1800. The strength of the peak existing
in the region of 1,570-1,620 cm
-1 and the strength of the peak existing in the region of 1,350-1,370 cm
-1 were measured, and the R value obtained therefrom and the Δυ value, which is the
half-value width of the peak existing at 1,570-1,620 cm
-1, were determined.
[0065] The charging and discharging capacity of the negative electrode, the rate characteristics
against high-speed charge and discharge, and the electro-chemical determinations such
as determination of the potential-capacity curve, were conducted in the manner described
below.
[0066] A coin-type battery was prepared using a negative electrode material molded into
a sheet with a binder, a separator, an electrolyte and a lithium metal for the opposite
electrode, and it was evaluated by a commercial charge/discharge tester.
[0067] The sheet electrode was prepared in the following way. To 5 g of the electrode material,
a dimethylacetamide solution of polyvinylidene fluoride (PVdF) was added in an amount
of 10 wt% calculated as solids to form a slurry, and this slurry was coated on a copper
foil and preliminarily dried at 80°C. A 20 mm-diameter disc was punched from the coated
copper foil and dried under reduced pressure at 110°C to prepare an electrode.
[0068] A lithium metal electrode was disposed in opposition to the thus obtained electrode,
with an electrolyte-impregnated polypropylene-made separator interposed therebetween
to prepare a 2016 coin-type cell, and it was subjected to a charge and discharge test.
The electrolyte was prepared by dissolving lithium perchlorate in a ratio of 1.0 mol/L
into an ethylene carbonate/diethyl carbonate (1:1 by volume) mixed solvent.
[0069] In the standard charge/discharge test, doping was carried out until the interpole
potential difference became 0 V at a current density of 0.16 mA/cm
2, while undoping was conducted until the interpole potential difference became 1.5
V at a current density of 0.33 mA/cm
2
[0070] In the test of rate characteristics against high-speed charge and discharge, doping
was carried out until the interpole potential difference became 0 V at a current density
of 0.16 mA/cm
2, while undoping was conducted until the interpole potential difference became 1.5
V at a current density of 5.6 mA/cm
2.
[0071] The capacity was evaluated by conducting the charge/discharge test on each of the
three coin-type cell samples, determining the efficiency of the first cycle, which
is the ratio of doping capacity to undoping capacity in the first cycle, the doping
and undoping capacities in the fourth cycle, and the undoping capacities at 2.8 mA/cm
2 and 5.6 mA/cm
2, and averaging the determinations.
Examples 1-8
[0072] The procured graphite material was screened to obtain the material having an average
particle size (measured in the manner described above) of 4 to 40µm. Then the BET
specific surface area of the particles of thus obtained graphite material was measured,
and the particles having a specific surface area of not more than 25 m
2/g were selected.
[0073] Finally, the particles satisfying the conditions of the above-shown formula (I) or
(II) in the relation between the BET specific surface area "y" and the particle size
"x" were selected and used as the carbonaceoous negative electrode for a lithium ion
secondary battery.
[0074] The thus obtained battery was subjected to the said standard charge/discharge test.
The results are shown in Tables 1 and 2.
Comparative Examples 1-6
[0075] The lithium ion secondary batteries were made according the same procedure as defined
in Example 1 except that a graphite powder satisfying the conditions of the formula
(I) or (II) on the relation between BET specific surface area "y" and particle size
"x" was used as electrode material, and these batteries were subjected to the same
standard charge/discharge test as conducted in Example 1. The results are shown in
Tables 1 and 2.
Example 9
[0076] A negative electrode was made in the same way as defined in Example 1 except that
the graphite material was calcined in an inert gas atmosphere at 2,000°C, and the
same evaluations as defined in Example 1 were conducted. The results are shown in
Tables 1 and 2.
Example 10
[0077] 2.0 kg of the same artificial graphite power as used in Example 8 and 1.0 kg of ethylene
heavy end tar (EHE, produced by Mitsubishi Chemical Corporation.), which is a naphtha
cracking product, were mixed in a stainless tank having an internal capacity of 20
litres, and the obtained slurry-like mixture was heated to 1,100°C in a batch-type
heating oven under an inert atmosphere and maintained in this state for 2 hours. The
resulting product was pulverized and passed through a vibrating screen to select the
particles having a size of 18 to 22 µm, finally obtaining an "amorphous carbon-coated
graphitic carbonaceous material", or a graphitic carbonaceous material having its
particle surfaces coated with 7 wt% of amorphous carbon. A lithium ion secondary battery
was prepared in the same way as in the preceding Examples except that the said "amorphous
carbon-coated graphic carbonaceous material" was used as the negative electrode, and
this battery was subjected to the same standard charge/discharge test as conducted
in the preceding Examples. The results are shown in Table 3.
Example 11
[0078] A negative electrode was prepared in the same way as defined in Example 10 except
for use of the artificial graphite used in Example 4. The evaluation results are shown
in Table 3.
Comparative Example 7
[0079] A negative electrode was prepared in the same way as defined in Example 10 except
for use of the artificial graphite used in Comparative Example 3. The evaluation results
are shown in Table 3.
Example 12
[0080] 3.0 kg of an artificial graphite powder and 1.0 kg of ethylene heavy end tart (EHE,
produced by Mitsubishi Chemical Corporation), a naphtha cracking product, were mixed,
and the obtained slurry-like mixture was devolatilized by heating at 700°C under an
inert atmosphere in a batch-type heating oven for one hour, then heated to 1,300°C
and maintained in this state for 2 hours. The thus treated mixture was pulverised
and passed through a vibrating screen to select the particles having a size of 20
to 25 µm. These particles were fed into 12.5 litres of 5 N hydrochloric acid and stirred
for 3 days. Then hydrochloric acid was filtered away and the residual precipitate
was washed with pure water. This operation was repeated until pH of the washing water
holding the precipitate in a dispersed state returned to neutrality. The obtained
precipitate was dried by heating at 120°C and used as the carbonaceous negative electrode
for a lithium ion secondary battery, and this battery was subjected to the same standard
charge/discharge test as conducted in the preceding Examples. The results are shown
in Table 4.
Example 13
[0081] A negative electrode was prepared in the same way as defined in Example 12 except
for use of 7 N hydrochloric acid. The evaluation results are shown in Table 4.
Example 14
[0082] A negative electrode was prepared in the same way as defined in Example 12 except
for use of 5 N sodium hydroxide The evaluation results are shown in Table 4.
Example 15
[0083] A negative electrode was prepared in the same way as defined in Example 12 except
for use of 13 N nitric acid. Tile evaluation results are shown in Table 4.
Example 16
[0084] A negative electrode was prepared in the same way as defined in Example 12 except
for use of 2.5 N oxalic acid. The evaluation results are shown in Table 4.
Comparative Example 8
[0085] A negative electrode was prepared in the same way as defined in Example 12 except
that an artificial graphite powder was used as electrode material without giving any
treatment thereto. The evaluation results are shown in Table 4.
Comparative Example 9
[0086] The same artificial graphite powder as used in Example 2 was supplied into 12.5 litres
of 5 N hydrochloric acid and stirred for 3 days, after which hydrochloric acid was
filtered away and the residual precipitate was washed with pure water. This operation
was repeated until pH of the washing water holding the precipitate in a dispersed
state returned to neutrality. The obtained precipitate was dried by heating at 120°C
and used as negative electrode material for a lithium ion secondary battery, and this
battery was subjected to the same standard charge/discharge test as conducted in the
preceding Examples. The results are shown in Table 4.
Comparative Example 10
[0087] 1.0 kg of the same ethylene heavy end tar as used in Example 12 was heat-treated
at 700°C under an inert atmosphere in a batch-type heating oven for one hour for devolatilization,
then heated to 1,300°C and maintained in this state for 2 hours, after which this
material was pulverized and passed through a vibrating screen to select the particles
having a size of 20 to 25 µm. Then hydrochloric acid was filtered away and the residual
precipitate was washed with pure water. This operation was repeated until pH of the
washing water holding the precipitate in a dispersed state returned to neutrality.
The obtained precipitate was dried by heating at 120°C and used as negative electrode
material of a lithium ion secondary battery, and this battery was subjected to the
same standard charge/discharge test as conducted in the preceding Examples. The results
are shown in Table 4.
Comparative Example 11
[0088] The same ethylene heavy end tar as used in Example 12 was devolatilized by heating
at 1,300°C under an inert atmosphere in a batch-type heating oven for 2 hours, then
pulverized, passed through a vibrating screen to select the particles having a size
of 20 to 25 µm, and used as negative electrode material for a lithium ion secondary
battery, and this battery was subjected to the same standard charge/discharge test
as conducted in the preceding Examples. The results are shown in Table 4.
Table 1
| |
Type of graphite |
1st cycle efficiency (%) |
Doping capacity (mAh/g) |
| Example 1 |
Natural graphite |
89 |
365 |
| Example 2 |
Natural graphite |
91 |
360 |
| Example 3 |
Natural graphite |
90 |
362 |
| Example 4 |
Artificial graphite |
91 |
348 |
| Example 5 |
Kish graphite |
90 |
364 |
| Example 6 |
Artificial graphite |
88 |
334 |
| Example 7 |
Natural graphite |
85 |
339 |
| Example 8 |
Artificial graphite |
89 |
345 |
| Example 9 |
Artificial graphite |
88 |
335 |
| Comparative Example 1 |
Natural graphite |
95 |
320 |
| Comparative Example 2 |
Natural graphite |
91 |
345 |
| Comparative Example 3 |
Artificial graphite |
89 |
301 |
| Comparative Example 4 |
Artificial graphite |
91 |
303 |
| Comparative Example 5 |
Artificial graphite |
81 |
320 |
| Comparative Example 6 |
Artificial graphite |
86 |
282 |
| |
Undoping capacity (mAh/g) |
Capacity at 2.8 mA/cm2 (mAh/g) |
Capacity at 5.6 mA/cm2 (mAh/g) |
| Example 1 |
363 |
362 |
334 |
| Example 2 |
356 |
350 |
313 |
| Example 3 |
360 |
356 |
347 |
| Example 4 |
348 |
341 |
285 |
| Example 5 |
365 |
368 |
364 |
| Example 6 |
349 |
327 |
256 |
| Example 7 |
338 |
321 |
206 |
| Example 8 |
342 |
330 |
269 |
| Example 9 |
345 |
342 |
335 |
| Comparative Example 1 |
320 |
237 |
106 |
| Comparative Example 2 |
342 |
314 |
164 |
| Comparative Example 3 |
299 |
260 |
100 |
| Comparative Example 4 |
301 |
267 |
75 |
| Comparative Example 5 |
317 |
312 |
266 |
| Comparative Example 6 |
280 |
271 |
223 |
Table 2
| |
Average particle size (µm) |
Specific surface area (m2/g) |
R value |
Δυ value (cm-1) |
| Example 1 |
17.0 |
6.1 |
0.13 |
17.8 |
| Example 2 |
14.0 |
4.9 |
0.09 |
19.2 |
| Example 3 |
12.2 |
8.8 |
0.05 |
19.1 |
| Example 4 |
24.0 |
5.0 |
0.11 |
20.6 |
| Example 5 |
14.2 |
4.9 |
0.02 |
20.0 |
| Example 6 |
7.9 |
12.9 |
0.16 |
21.1 |
| Example 7 |
6.3 |
16.1 |
0.20 |
21.2 |
| Example 8 |
17.0 |
8.9 |
0.15 |
22.2 |
| Example 9 |
8.0 |
9.8 |
0.05 |
20.3 |
| Comparative Example 1 |
40.7 |
2.4 |
0.08 |
20.3 |
| Comparative Example 2 |
19.7 |
12.1 |
0.23 |
22.6 |
| Comparative Example 3 |
18.0 |
10.3 |
0.29 |
24.6 |
| Comparative Example 4 |
14.0 |
12.8 |
0.41 |
25.9 |
| Comparative Example 5 |
6.7 |
21.1 |
0.28 |
25.5 |
| Comparative Example 6 |
9.1 |
15.6 |
0.34 |
26.5 |
Table 3
| |
Example 10 |
Example 11 |
Comparative Example 7 |
| Treating solution |
None |
None |
None |
| First cycle efficiency (%) |
92 |
92 |
92 |
| Doping capacity (mAh/g) |
350 |
362 |
315 |
| Undoping capacity (mAh/g) |
348 |
361 |
314 |
| Capacity at 2.8 mA/cm2 (mAh/g) |
334 |
348 |
280 |
| Capacity at 5.6 mA/cm2 (mAh/g) |
300 |
312 |
130 |
Table 4
| |
Treating solution |
1st cycle efficiency (%) |
Doping capacity (mAh/g) |
| Example 12 |
5 N hydrochloric acid |
95 |
386 |
| Example 13 |
7 N hydrochloric acid |
94 |
378 |
| Example 14 |
5N NaOH |
93 |
356 |
| Example 15 |
13 N nitric acid |
93 |
356 |
| Example 16 |
2.5 N oxalic acid |
92 |
348 |
| Comparative Example 8 |
none |
92 |
352 |
| Comparative Example 9 |
5 N hydrochloric acid |
94 |
354 |
| Comparative Example 10 |
5 N hydrochloric acid |
84 |
222 |
| Comparative Example 11 |
none |
88 |
215 |
| |
Undoping capacity (mAh/g) |
Capacity at 2.8 mA/cm2 (mAh/g) |
Capacity at 5.6 mA/cm2 (mAh/g) |
| Example 12 |
384 |
308 |
300 |
| Example 13 |
378 |
379 |
350 |
| Example 14 |
354 |
353 |
326 |
| Example 15 |
354 |
353 |
326 |
| Example 16 |
346 |
338 |
282 |
| Comparative Example 8 |
350 |
336 |
290 |
| Comparative Example 9 |
354 |
298 |
127 |
| Comparative Example 10 |
220 |
206 |
184 |
| Comparative Example 11 |
213 |
200 |
168 |
[0089] The foregoing results confirm that the lithium ion secondary batteries according
to the present invention (1) can develop a doping capacity close to the theoretical
lithium ion occlusion capacity (372 mAh/g) of graphite, (2) shows a high undoping
capacity and a high first cycle efficiency, and (3) can maintain a high capacity even
during high-speed charge and discharge at 2.8 mA/cm
2 and 5.8 mA/cm
2. It is also noted that the lithium ion secondary batteries of the present invention
according to Examples 12 and 13 have a doping capacity and an undoping capacity which
exceed the theoretical lithium ion occlusion capacity of graphite.